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(11) | EP 0 029 715 A1 |
| (12) | EUROPEAN PATENT APPLICATION |
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| (54) | Porous spherical carbonaceous product and production thereof |
| (57) Problems with conventional porous spherical carbon particles used to absorb endogenous
toxins in the intestines of mammals, such as bile acids coating the surface of the
particles, are now overcome by the use of a porous and spherical carbonaceous product
having acidic, basic, phenolic hydroxyl and carboxyl functional groups wherein the
ratio of equivalents of acidic groups to equivalents of basic groups is 0.40:1 to
2.5:1 and the value obtained by subtracting the equivalents of carboxyl groups from
the sum of the equivalents of basic groups and phenolic hydroxylic groups is greater
than 0.60 equivalent/kg of the product. The product can be used to treat diseases
of the liver or kidney. |
[0001] The present invention relates to a porous and spherical carbonaceous product having acidic, basic, phenolic hydroxyl and carboxyl functional groups and to a method of preparing this product.
[0002] In recent years, a method of removing toxic substances within living bodies by a hemodialyzer as an artificial organ has prevailed with increased cases of disease due to troubles in renal and hepatic functions. However, skilled specialists are required for operation of the complicated apparatus of a hemodialyzer. There is a high physical and mental strain for the patient because it is necessary to take the patient's blood out from his body. The method is relatively expensive.
[0003] A method of removing endogenous toxins formed due to liver and kidney diseases within the living body by internal administration of an orally administered pharmaceutical substance, for instance oxidized starch, has recently been proposed. However, the proposed medicine is a reactive substance. Although it is able to remove intestinal urea, it cannot remove the essentially endogenous toxins caused by the liver and kidney diseases such as octopamine, beta-amino-isobutyric acid and dimethylamine. It also has a side- reaction of stimulating the intestinal wall. Accordingly, use of such a medicine is not preferable.
[0004] On the other hand, in view of the favourable properties of medicinal activated carbon such as its adsorption of various substances and its safety to living bodies, trials for the removal of the endogenous toxins caused by liver and kidney diseases have been carried out using such carbon. However, although . the carbon is useful as an antidote which adsorbs and removes gastrointestinal toxic substances taken from the mouth, it has insufficient ability to remove the endogenous toxins in the intestines due to diseases of the liver and kidney. This is because of the presence of substances such as bile acids which coat the surface of active carbon and interfere with the activity of the carbon. In addition, the carbon is apt to cause constipation after oral administration and this constipation can be particularly dangerous to patients suffering from liver or kidney diseases.
[0005] It has now been found that these problems can be overcome by using a porous and spherical carbonaceous product containing specified functional groups in specified mutual relationships. The product exhibits an excellent absorptive effect on endogenous toxins caused by liver and kidney diseases, even in the presence within the intestinal tracts of bile acid, while not absorbing digestive enzymes in the gastrointestinal tracts and not causing symptoms of constipation. The present invention therefore provides a spherical and carbonaceous product having acidic, basic, phenolic hydroxyl and carboxyl functional groups wherein the ratio of equivalents of said acidic groups to equivalents of said basic groups is from 0.40:1 to 2.5:1 and the value obtained by subtracting the equivalents of said carboxyl groups from the sum of the equivalents of said basic groups and the equivalents of said phenolic hydroxyl groups is greater than 0.60 equivalent/kg.
[0006] The product of the invention can be prepared by a method in which a first porous spherical carbonaceous substance is heated at a temperature of 350 to 700°C in an atmosphere containing 0.5 to 20% by volume of oxygen or an oxygen-containing gas, and further heated at a temperature of 800 to 1000°C in an atmosphere inert to carbon.
[0007] The porous and spherical carbonaceous product of the present invention has, as functional groups, acidic groups, basic groups, phenolic hydroxyl groups and carboxyl groups in the following mutual relationships:
(1) the ratio of equivalents of the acidic groups to the equivalents of the basic groups is in the range of 0.40:1 to 2.5:1, and
(2) the value obtained by subtracting the equivalents of carboxylic groups from the sum of the equivalents of the basic groups and the phenolic hydroxyl groups is larger than 0.60.
[0008] When the amounts of the acidic, basic, phenolic hydroxyl and carboxyl groups are represented respectively by A, B, C and D equivalent/kg of the material (hereinafter referred to as eq/kg), the relationships become as follows:
and
[0009] Preferably, the product of the present invention contains the above-mentioned functional groups in the amounts shown below:
a) Acidic group (A group)
[0011] After adding 10-3kg (one gram) of a pulverized specimen of the product of the present invention passing through a Taylor standard sieve of 200 mesh to 5 x 10- m3 (50 ml) of an aqueous 0.05 N NaOH solution and shaking the mixture for 48 hours, the mixture is filtered to remove the specimen. The filtrate is titrated to neutrality. The amount of A groups is represented by the amount of NaOH consumed by the specimen expressed as eq/kg of the specimen.
b) Basic group (B group)
[0012] After adding 10-3kg (one gram) of a pulverized specimen of the product of the present invention passing through a Taylor standard sieve of 200 mesh to 5 x 10-5 m3 (50 ml) of an aqueous 0.05 N HC1 solution and shaking the mixture for 24 hours, the mixture is filtered to remove the specimen. The filtrate is titrated to neutrality. The amount of B groups is represented by the amount of HCl consumed by the specimen expressed as eq/kg of the specimen.
c) Phenolic hydroxyl group (C group)
[0013] After adding 10-3kg (one gram) of a pulverized specimen of the product of the present invention passing through a Taylor standard sieve of 200 mesh to 5 x 10-5m3(50 ml) of an aqueous 0.05 N Na2C03 solution and shaking the mixture for 24 hours, the mixture is filtered to remove the specimen. The filtrate is titrated to neutrality. The amount of C groups is represented by the balance obtained by subtracting the amount of Na2C03 consumed by the specimen from the amount of acidic groups, expressed as eq/kg of the specimen.
d) Carboxyl group (D group)
[0014] After adding 10-3kg (one gram) of a pulverized specimen of the product of the present invention passing through a Taylor standard sieve of 200 mesh to 5 x 10-5m3 (50 ml) of an aqueous 0.05 N NaHCO3 solution and shaking the mixture for 24 hours, the mixture is filtered to remove the specimen. The filtrate is titrated to neutrality. The amount of D groups is represented by the amount of NaHCO3 consumed by the specimen, expressed as eq/kg of the specimen.
[0015] The fact that the specified relationships between the various functional groups is specific to the product of the present invention can be understood from Table 1. In this Table the above-mentioned specified relationships are compared with those of a commercial spherical activated carbon having the same shape.
[0016] The porous and spherical carbonaceous substance according to the present invention preferably consists of porous and spherical particles of 5 x 10-5 to 10-3m (0.05 to 1 mm) in diameter, a specific pore volume for pores with radii of less than 8 x 10-9m (80 A) of 2 x 10-4 to 10-3m3/kg (0.2 to 1.0 cc/g) and a specific pore volume for pores with radii of 10-8 to 7.5 x 10-6m (100 to 75,000 A) of 10-4 to 10-3m3 /kg (0.1 to 1.0 cc/g). The specific pore volume for pores with radii of less than 8 x 10-9m (80 A) is determined by a conventional gas adsorption method, and that for pores with radii of 10-8 to 7.5 x 10-6m3 (100 to 75,000 A) is determined by a mercury porosimeter.
[0017] The porous and spherical carbonaceous product according to the present invention can be produced by the following method:
(a) Preparation of a spherical carbonaceous substance as a precursor of the product of the present invention.
[0018] A heavy hydrocarbon of a ratio of H/C of 0.45 to 0.80 and of a flow point of 100 to 300°C, in which the presence of unevenly distributed anisotropic regions is not observed under a polarization microscope, is used as the starting material. A mixture of this heavy hydrocarbon and an aromatic hydrocarbon such as benzene and naphthalene is dispersed in hot water, preferably at a temperature of 100 to 180°C, containing a surfactant while stirring the mixture of the hydrocarbons and hot water to shape minute particles of the mixture of hydrocarbons. After cooling the dispersion to room temperature, the thus formed and solidified minute particles are separated from the greater part of the aqueous phase by filtration. The aromatic hydrocarbon contained in the minute particles is removed by extraction with an organic solvent such as hexane or methanol. The thus extracted particles are brought into contact with a flow of an oxidative gas, for instance an oxygen flow, to effect oxidation of the minute particles. The content of oxygen in the resulting particles is 7 to 25% by weight. Then, the thus partially oxidized minute particles are heated in a flow of a gas having a reactivity to carbon at high temperatures, such as steam and gaseous carbon dioxide, at a temperature of 800 to 1000°C to convert the particles into a porous and spherical carbonaceous substance.
(b) Production of the present product
[0019] The porous and spherical carbonaceous substance obtained above is heated at a temperature of 350 to 700°C, preferably at 400 to 600°C in an atmosphere containing 0.5 to 20% by volume, preferably 3 to 10% by volume, of oxygen, and is then further heated at a temperature of 800 to 1000°C in an atmosphere of a gas inert to carbon, for instance nitrogen, argon or helium or of a mixture of such inert gases to obtain the porous and spherical carbonaceous substance of the present invention. The atmosphere containing oxygen can be formed by using oxygen, nitrogen oxides or air as the oxygen source. '
[0020] The series of heat-treatments described above confers on the spherical carbonaceous substance a balance between the adsorbency of acidic and basic substances as well as an adsorbency to amphoteric substances. In addition, the heat-treatments confer on the porous and spherical carbonaceous substance the selective adsorbing sites expressed by "the ratio of equivalents of the acidic groups to equivalents of the basic groups" and "the value obtained by subtracting the equivalents of the carboxylic groups from the sum of the equivalents of the basic groups and the phenolic hydroxyl groups: (B + C) - D".
[0021] Heat-treatment in an atmosphere containing oxygen only may improve the adsorptive ability to basic substances such as amine. However, the adsorptive ability to the amphoteric substance can not be improved in this way.
[0022] The spherical carbonaceous substance of the present invention exhibits a specific adsorptive ability to endogenous toxins within the living bodies, as will be described later, which could not be presumed from the adsorptive ability of conventional activated carbon. Although the adsorption mechanism has not yet been elucidated, it is presumed to be due to the selectivity of the adsorption sites caused by the specified relationships among the various functional groups on the internal surface of the porous and spherical carbonaceous substance and the synergistic function of the charged potential on the outer surface and of the minute physical structure of the product of the invention.
[0023] The product of the present invention can be used in treating liver and/or kidney diseases, especially diseases aggravated and/or caused by endogenous toxin(s) in the intestines of a human or mammal. It is possible for the present product to exhibit an adsorptive ability which has hitherto not been demonstrated in activated carbon including conventional carbons for pharmaceutical use. The present product exhibits its adsorptive ability to endogenous toxins even in the presence of bile acids. In other words, the present product effectively adsorbs octopamine and gamma- aminobutyric acid which are the causal substance of hepatic encephalopathy, endogenous toxins and their precursors in kidney diseases, for example watersoluble basic and amphoteric substances such as dimethylamino beta-amino-isobutyric acid, asparatic acid and arginine. In addition, the present product adsorbs only a little of the digestive enzymes within the intestines, which preferably ought not to be removed. Moreover, it does not cause constipation.
[0024] Accordingly, the present product can work well in the treatment of tremor and cerebral disorders due to liver diseases and in the treatment of metabolic abnormality and functional abnormality, and in the improvement of light renal disorder before hemodialysis in kidney diseases and of the conditions during hemodialysis. In addition, it can work well in the treatment of other diseases, for example psychosis due to noxious substances within the living body.
[0025] Where the present product is applied as a medicine for treating diseases of the liver and/or kidney, its dose depends on the patient concerned, such as whether the patient is human or another mammal, the age of the patient, and the particular condition of the patient. In humans, the usual oral dose is 10 -3 to 5 x 10-3kg (1 to 5g)/day taken in 3 or 4 portions during the day. However, the dose is dependent on the factors explained above and may be increased or decreased as appropriate.
[0026] The present product may take any one of several shapes and forms when it is to be administered as a medicine. The product may be in the form of particles, granules, tablets, sugar-coated tablets, capsules or a suspension. In the case where it is administered as capsules, gelatin and/or other substances which dissolve within the intestines can be used to encapsulate the product. In the cases of using tablets, it is necessary for the tablets to disintegrate into the original minute spherical particles of the product of the invention within the body of a patient. In addition, the present product may be combined with an electrolyte- controlling agent such as aluminum gel or KAYEXALATE (produced by Winthrop Lab., USA) and administered as a combined medicine.
[0027] The product of the present invention has an extremely low toxicity to mammals as can be seen below:
A. Acute toxicity test in mammals:
[0028] Each of the porous and spherical carbonaceous substances of the present invention prepared in Examples 1, 2 and 3 below was administered via a stomach tube to a respective group of male and female JCL-SD rats (average body weight of 8.78 x 10-2 + 4.3 x 10 3kg (87.8 ± 4.3 g) for female rats, and of 9.78 x 10-2 + 4.0 x 10 3 kg (97.8 + 4.0 g) for male rats). Each group consisted of 10 animals of one sex. After one week of observations, no death was recorded. When autopsies were carried out after the end of the period of observation, no abnormal findings were obtained from external or from internal observation on several organs as well as no noticeable symptoms of intoxication due to the administration. The respective LD50 values of the products of the invention that were tested are shown in Table 2.
B. Sub-acute toxicity test on mammals:
[0029] Five kinds of different solid diets were given for one month to 10 groups of JCL-SD rats of age 4 weeks. Each group consisted of either 10 males or 10 females and each diet was fed to 1 group of males and 1 group of females. The five kinds of diet respectively contained 0, 1, 2, 5 and 10% by weight of the product of Example 3 below. The diet and water were taken ad lib. During the period of administration of the diet, the amounts of water and the diet taken by the rats and the body weight of the rats were measured, and their behaviour was observed.
[0030] After the period of administration was over, blood specimens were collected from the rats and then the rats were sacrificed to be autopsied. The average amount of diets taken by the rats during the period of adminstration was as follows, respectively corresponding to the content of the present product of 1, 2, 5 and 10% by weight: 1100, 2300, 5700 and 11400 10-6kg/kg (mg/kg) body weight of female rat, and 1400, 2800, 7000 and 14000 10-6kg/kg (mg/kg) body weight of male rat.
[0031] Although a slight suppression of body weight gain was observed in the middle stage of the test on the group of male rats which took the diet of the highest content of the product of the invention, body weight recovered afterwards. Except for this finding, no noticeable abnormal findings were obtained for body weight gain, the general conditions, blood examination, urinalysis, autopsy, weight of organs and pathohistological examination of various tissues as well as symptoms of intoxication.
EXAMPLE 1
[0033] 3 x 10-1kg (three hundred grams) of a heavy hydrocarbon of H/C of 0.55, a flow point of 220°C and not having localized presence of an anisotropic region under a polarization microscope, and 10" kg (100 g) of naphthalene were introduced into an autoclave provided with a stirrer. The mixture was further mixed well at a temperature of 180°C. Into the thus obtained liquid mixture, 1.2 kg (1200 g) of an aqueous 0.5% solution of polyvinyl alcohol (degree of saponification of 88%) were added. Then, the mixture was vigorously stirred at a temperature of 140°C for 30 min and cooled to room temperature while stirring to form a dispersion of spherical particles of from 7 x 10 5 to 1.2 x 10-3m (0.07 to 1.2 mm) in diameter. After separating the greater part of the water from the spherical particles, the particles were treated with hexane in an extractor to remove naphthalene contained in the particles by extraction, and dried by air flow. The resulting particles were heated to 300°C at a rate of temperature rise of 25°C/hour by a flow of heated air in a fluidized bed system and further heated for 2 hours at a fixed temperature of 300°C. Spherical particles containing 14% by weight of oxygen were obtained. These particles were heated to a temperature of 900°C by steam in a fluidized bed system. The particles were heated for two hours at this temperature to obtain the porous and spherical carbonaceous particles which are the precursor of the product of the present invention.
[0034] The precursor particles were heated to a temperature of 600°C in an atmosphere containing 3% by volume of oxygen, and heated for a further 3 hours in the same atmosphere. Then, the precursor particles were further heated to a temperature of 950°C in an atmosphere of nitrogen and kept at that temperature for 30 min in an atmosphere of nitrogen to obtain the product of the present invention. The properties and the content of the various functional groups in this product are shown in Table 3.
EXAMPLE 2
[0035] 3 x 10-1kg (three hundred grams) of a heavy hydrocarbon of H/C of 0.65 and of a flow point of 210°C and 10" kg (100 g) of naphthalene were introduced into an autoclave provided with a stirrer and co-melted by heating to a temperature of 180°C while stirring. 1.2 kg (1200 g) of an aqueous 0.5% solution of polyvinyl alcohol of a degree of saponification of 88% was added to the liquid mixture thus-obtained. The resulting mixture was agitated vigorously at a temperature of 130°C for 30 min. On cooling the mixture to room temperature while stirring, an aqueous dispersion of spherical particles of from 10 to 1.3 x 10-3m (0.1 to 1.3 mm) in diameter was obtained. After removing a greater part of the water from the spherical particles, the particles were treated with hexane in an extractor to remove naphthalene from the particles by extraction. The particles from which naphthalene had been removed were dried by air flow, and heated to a temperature of 300°C by heated air in a fluidized bed system at a rate of temperature rise of 25°C/hour, and then further heated for 2 hours at 300°C. Spherical particles containing 20% by weight of oxygen were obtained. These particles were heated to a temperature of 900°C in steam by a fluidized bed system and kept at 900°C for 2 hours in steam to be converted into a porous and spherical carbonaceous substance which is the precursor of the present product. Then, the precursor particles were kept at a temperature of 450°C for 4 hours in an atmosphere containing 10% by volume of oxygen. The particles were further heated to a temperature of 800°C in an atmosphere of nitrogen and kept at 800°C for 30 min in this atmosphere to obtain the present product. The adsorbing property of and the amount of the various functional groups in the product are shown in Table 3.
EXAMPLE 3
[0036] The spherical particles containing 14% by weight of oxygen which had been obtained in the course of Example 1 were heated to a temperature of 900°C in', steam by using a fluidized bed system and kept at 900°C for 2 hours in steam to obtain a porous and spherical carbonaceous substance as a precursor of the present product. The precursor particles were kept at a temperature of 550°C in an atmosphere containing 3% by volume of oxygen for 5 hours. The particles were then heated to a temperature of 900°C in an atmosphere of nitrogen and kept at 900°C for 30 min in this atmosphere to obtain the present product. The adsorbing property of and the amount of the various functional groups in the product are shown in Table 3.
Comparative Example
[0037] The spherical particles containing 14% by weight of oxygen which had been obtained in the course of Example 1 were heated to 900°C in steam by a fluidized bed system and kept at 900°C for a further 2 hours to obtain a porous spherical carbonaceous substance. This substance was further heated at a temperature of 550°C in an atmosphere containing 3% by volume of oxygen for 5 hours to obtain a porous and spherical carbonaceous substance. The adsorbing property of and the amount of the various functional groups in this latter substance are shown in Table 3.
EXAMPLE 4
[0038] The present Example is concerned with the results of a determination of the adsorptive property and the content of the specified functional groups of the porous and spherical carbonaceous substances produced in Example 1 to 3 and in the Comparative Example, and of a commercial spherical activated carbon for use in hemoperfusion. The adsorptive property was determined on beta-amino-isobutyric acid, gamma- aminobutyric acid, dimethylamine and octopamine in the presence of bile acid in vitro. The results are shown in Table 3. The amount of adsorbed substance is expressed by the adsorbed amount (kg/1000 kg) (mg/g) when the specimen was put into an aqueous solution of the above-mentioned substance at a concentration of 50 kg/m (5 mg/dl) in the presence of bile acids of a concentration of 0.5% by weight in the aqueous solution.
[0039] As is seen in Table 3, it is clear that the adsorptive property of the present product, that is the porous and spherical carbonaceous substance of the present invention having the specified functional groups in the specified mutual relationships, is far superior to that of the product of the Comparative Example or the commercial spherical activated carbon hitherto used for hemoperfusion in the treatments of diseases of the liver and kidney.
EXAMPLE 5
[0040] The present Example shows the efficacy of treatment with the present product of experimental animals suffering from an experimental renal failure.
[0041] Three groups of female JCL-SD rats of body weight of 1.8x10 1 to 2.2x10-1 kg (180 to 220 g), (each group consisting of 10 animals) were incised transversally of their abdomen under anaesthesia. The renal hilums of one of the kidneys of each animal was ligated. After suturing the incised part and naturalizing the rat for one week, the same operation was carried out on the other kidney to prepare the groups of rats suffering from experimental renal failure. While giving diet and water taken ad lib, the porous and spherical carbonaceous substance of the invention prepared in Example 3 was forcibly administered to the rats of a first group orally by a stomach tube at a daily dose of 5 kg/1000 kg (5000 mg/kg), and the product of the Comparative Example was administered to the rats of a second group in the same manner. The rats of a third group were administered nothing. The state of the rats of the three groups was observed to find the survival period (days) after the second operation. The results are shown in Table 4. As is seen in Table 4, the survival period of the group to which the product of Example 3 was administered was clearly longer than those of the groups of rats which were treated with the product of the Comparative Example and with nothing, respectively.
EXAMPLE 6
[0042] This Example is concerned with the treatment of a human patient with renal failure with the product of the present invention.
[0043] The patient, a man of age 44, suffering from chronic renal failure showed a level of creatinine of 20 to 40 kg/m3 (2 to 4 mg/dl) for a long time, afterwards a raised level of creatinine of 80 kg/m (8 mg/dl) after one month and then a still further raised level of creatinine of 110 kg/m3 (11 mg/dl) after two months accompanied by the subjective symptoms of loss of appetite and tiredness. The product prepared in Example 3 was then administered to the patient in the form of gelatin capsules by internal administration at a daily dose of 3x 10 3 to 4x10-3 kg (3 to 4 g) for six months.
[0044] The level of creatinine of the patient began to show a reduction 2 weeks after the commencement of the treatment and stabilized at 80 kg/m to 90 kg/m (8 to 9 mg/dl) together with the substantial disappearance of his subjective symptoms.
EXAMPLE 7
[0046] A woman of age 72 suffering from a liver disease, showing a persistent concentration of ammonia in her blood of 2.5x10-3 to 3.0x10-3 kg/m3 (250 to 300 micrograms/dl) and having disturbances of consciousness once a month was treated by internal administration of the product of the invention produced in Example 3 at a daily dose of 5x10-3kg (5g) encapsulated in gelatin capsules for 3 months. During the period of treatment, the disturbances of consciousness never occurred and the concentration of ammonia in her blood reduced to 1.5x10-3 kg/m3 (150 micrograms/dl). After finishing the treatment, a light disturbance of consciousness attacked her after 10 days and the concentration of ammonia in her blood had increased to 2x10-3 kg/m3 (200 micrograms/ dl). During the period of treatment, the values of examination of her blood and biochemical examination of her blood showed no abnormality.
1. A porous and spherical carbonaceous product having acidic, basic, phenolic hydroxyl
and carboxyl functional groups characterized in that the ratio of equivalents of said
acidic groups to equivalents of said basic groups is from 0.40:1 to 2.5:1 and the
value obtained by subtracting the equivalents of said.carboxyl groups from the sum
of the equivalents of said basic groups and the equivalents of said phenolic hydroxyl
groups is greater than 0.60 equivalent/kg.
2. A porous and spherical carbonaceous product according to claim 1, characterized
in that said product contains 0.30 to 1.20, 0.20 to 0.70, 0.20 to 0.70, and more than
0.15 equivalent/kg of said product of said acidic groups, said basic groups, said
phenolic hydroxyl groups and said carboxyl groups respectively.
3. A porous and spherical carbonaceous product according to claim 1 or 2, characterized
in that said product consists of particles 5x10 5 to 10-3m in diameter.
4. A porous and spherical carbonaceous product according to any one of the preceding
claims for use in treating a disease aggravated and/or caused by endogenous toxin(s)
in the intestines of a mammal.
5. A method for producing a porous and spherical carbonaceous product as claimed in
any one of the preceding claims, characterized in that a first porous spherical carbonaceous
substance is heated at a temperature of 350 to 700°C in an atmosphere containing 0.5
to 20 % by volume of oxygen or an oxygen-containing gas, and further heated at a temperature
of 800 to 1000°C in an atmosphere inert to carbon.
6. A method according to claim 5 characterized in that said first porous spherical
carbonaceous substance is prepared by mixing an aromatic hydrocarbon with a heavy
hydrocarbon of an atomic ratio of hydrogen to carbon of 0.45:1 to 0.8:1 in which the
presence of an uneven distribution of anisotropic regions is not observable under
a polarization microscope, dispersing this mixture in hot water containing a surfactant
under agitation, thereby shaping said mixture into minute spherical particles, cooling
the resulting dispersion of particles, separating off said minute particles, extracting
said aromatic hydrocarbon from said minute particles, sieving said minute particles,
thereby collecting the minute particles of uniform size, bringing said minute particles
into contact with an oxidative gas flow, thereby obtaining minute particles containing
7 to 25 % by weight of oxygen, and heating the thus obtained minute particles containing
7 to 25 % by weight of oxygen at a temperature of 800 to 1000°C in a flow of a gas
or gaseous mixture reactive to carbon at high temperatures, thereby obtaining said
first porous spherical carbonaceous substance.